Modified X-Type Molecular Sieve for p-Xylene Mass Transfer
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Solution Overview
Problem
Existing methods for separating and purifying aromatic hydrocarbon isomers, such as p-xylene, are inadequate due to insufficient adsorption capacity and mass transfer performance of X-type molecular sieves, particularly in selective adsorption processes.
Innovation Solution
A modified X-type molecular sieve is developed with mesopore and macropore channels, created through hydrothermal treatment and treatment with NaOH, SiO2, and an organic ammonium salt, maintaining high micropore volume and enhancing mass transfer performance.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Reliability
If X-type molecular sieve is used for adsorptive separation of p-xylene, then selective adsorption capability is improved, but mass transfer performance deteriorates due to limited pore accessibility
Solution Approach 1:
The patent introduces mesopores (2-50 nm) and macropores (>50 nm) into the X-type molecular sieve structure through hydrothermal treatment with organic ammonium salts as structure-directing agents. This hierarchical pore structure maintains the micropore volume for selective adsorption while adding larger pores for improved mass transfer and accessibility of aromatic hydrocarbon isomers to active sites.
Solution Approach 2:
The patent transitions from a traditional single-scale micropore structure to a hierarchical multi-scale pore structure by incorporating mesopores and macropores alongside micropores. This dimensional expansion of pore size distribution enables simultaneous optimization of selectivity (via micropores) and mass transfer (via meso- and macropores).
2Quantity of substance
If micropore volume is increased to enhance adsorption capacity, then adsorption capacity is improved, but mass transfer efficiency deteriorates due to restricted diffusion pathways
Solution Approach 1:
The patent creates a hierarchical pore structure where micropores provide high adsorption capacity through increased micropore volume, while interconnected mesopores and macropores provide efficient diffusion pathways. The mesopores act as transport channels that facilitate rapid movement of aromatic hydrocarbons to micropore regions, resolving the trade-off between capacity and transfer efficiency.
Solution Approach 2:
The patent implements a nested pore structure where mesopores and macropores serve as outer transport channels that nest around and provide access to the inner micropore regions. This nested architecture allows large pores to facilitate mass transfer while small micropores provide adsorption capacity, with each scale serving its optimal function.
Applied Scientific Principles
This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.
Function Achieved in This Case
The modified X-type molecular sieve exhibits improved adsorption capacity and mass transfer performance, leading to enhanced separation efficiency of aromatic hydrocarbon isomers like p-xylene.
Implementation Method 1
X-type molecular sieve adsorbents exchanged with barium ions or barium and potassium ions have the property of selectively adsorbing p-xylene
Implementation Method 2
placing the X-type molecular sieve in a water vapor atmosphere to conduct hydrothermal treatment, preferably at a temperature of 250-550 °C for at least 0.5 hours
Data Source
Figure 1~2
Figure 3
AI summary
The present invention relates to a modified X-type molecular sieve, wherein the surface area of the modified X-type molecular sieve is 9.5-19 m2/g, and the sum of the mesopore and macropore volumes accounts for 6%-18% of the total pore volume; the present invention also relates to an adsorbent for aromatic hydrocarbon isomer containing the modified X-type molecular sieve, and their preparation method and use. The modified X-type molecular sieve and the adsorbent are used for adsorptive separation of p-xylene from mixed C8 aromatic hydrocarbons.